Magnesium calcium acetate products, and process for their manufacture

ABSTRACT

Finely divided ore blends containing chemically active magnesium oxide and calcium oxide are physically combined with a critical amount of water prior to reaction with acetic acid. Intermediate products range in physical consistency from putty-like masses to viscous liquors, depending upon the relative fraction of magnesium oxide in the ore feed. Intermediate products freeze to form hydrates of magnesium calcium acetate, the freeze times being dependent upon a number of chemical and physical parameters. Product drying requirements range from minimal drying to none at all, depending upon the magnesium fraction in the products. Products are non-friable and have excellent crush strength, and are suitable for storage, shipping and application in chemical deicing as well as other end use applications where crude low-cost materials are called for. 
     A unique situation centers around the composition corresponding to the magnesium mol fraction of 0.8. This material requires no drying and exhibits an extraordinary high crush strength. Additionally, as much as 75% by weight of traction agent (sand) can be successfully incorporated into this material without the aid of chemical binders.

BACKGROUND OF THE INVENTION

Calcium magnesium acetate has emerged in recent years as a viablenon-polluting replacement for salt, or sodium chloride, as a surfacedeicer. Research and development by the states as well as the FederalGovernment has focussed on compositions of lower magnesium content, inspite of the anticipation that higher magnesium content materials holdpromise as superior deicers. The blockage has been in the technology ofmanufacture. The present invention clears that blockage, and results inprocess innovations as well as new compositions known as magnesiumcalcium acetates.

DESCRIPTION OF PRIOR ART

In U.S. Pat. No. 4,606,836, I describe a commercially successful processfor the manufacture of calcium magnesium acetate deicer. The magnesiumcontent of the products in that case covered the mol fraction range0.5-0.67, where magnesium mol fraction is defined as follows: ##EQU1##The major reason for limiting X_(Mg) to 0.67 centered around the problemof incomplete chemical reaction of the magnesium-based raw material. AsX_(Mg) increased, the magnesium-based raw material, usually magnesiumoxide, or MgO, would tend to become encapsulated in product calciummagnesium acetate. More specifically, it was the hydrated magnesiumacetate component of the product mass which comprised a highly viscous,glassy material which seriously inhibited good contact between free(acetic) acid and MgO, raw materials.

It was clear in that case that the calcium-based raw material component,usually calcium oxide, or CaO, reacted more energetically with rawmaterial acetic acid. Thus the CaO component would react preferentiallywith the acid, and the MgO component reacted in a later stage.Additionally, the CaO reaction resulted in a large exotherm; this heatin turn helped to drive the reaction between MgO and acid.

Thus as the value of X_(Mg) increased in the attempted syntheses, twoevents occurred in concert to inhibit thorough reaction of the MgOcomponent:

1. raw material encapsulation decreased

2. the size of the exotherm decreased

The undesirable consequence of incomplete utilization of MgO rawmaterial is twofold. Firstly, the unreacted ore gives rise toundesirable insoluble matter when the deicer becomes dissolved in waterduring use. This would become a minor problem in areas where sewersystems receive the surface waters; these are the same areas where sandor other traction agents are proscribed beause of potential plugging ofsewer systems. Secondly and more important, unreacted raw materialacetic acid can become entrapped in the product which in turn producesan acid reaction in end use. It has been shown that a 10% calciummagnesium acetate solution in water must have a pH of at least 8 if itis not going to attack certain metals, or Portland cement concrete.

The mechanism of acid entrapment is the formation of the known compoundmagnesium acid-acetate, and/or calcium acid-acetate.

Even the phenomenon of acid entrapment can be handled, and that is byheating the product. Heat decomposes the acid-acetate(s) and drives offfree acetic acid, in addition to water. But product drying adds roughly15% to the capital cost of the production plant, and roughly 5% up tothe operating cost. Thus product drying is preferably avoided, andindeed is one of the key features of the instant invention.

The expedient of inputting less tha the stoichiometric requirement ofacetic acid, so as to avoid an acidic product, has been attempted. Thisapproach has been rejected, however, as it only leads to an escalationof the problem of residual insoluble MgO in the product. It also resultsin a waste of raw material ore.

Thus, for all the reasons given, successful manufacturing operationsinvolving products having an X_(Mg) value greater than 0.67 hadheretofore been frustrated. Yet there are compelling reasons forextending the X_(Mg) value beyond 0.67, indeed all the way to 1.0 whichcorresponds to magnesium acetate. Where such products are to be used asdeicers, these reasons are as follows:

1. The water-eutectics (freezing points) of solutions of these productsin water are substantially reduced as X_(Mg) moves from 0.67 to 1.0. Inessence, this means that the materials become superior deicers.

2. The rate of dissolution in water of these products increases asX_(Mg) moves from 0.67 to 1.0. This means that the deicers act morequickly when applied in an ice-melting siutation.

There are other end-uses for magnesium calcium acetate products whichcould benefit through an increase in the value of X_(Mg). For example, acrude low-cost magnesium acetate does not now exist on the market today,so that end uses are restricted to those which can support the cost ofthe refined magnesium acetate which is an article of commerce.

It is one object of the prior art to incorporate sand or other tractionagent into the calcium magnesium acetate particles. Whereas this hasbeen successful, as described in U.S. Pat. No. 4,606,836, there has beena limitation on the size of the particles which could in fact beproduced. For example, a product containing 75% sand seems to bepreferred by users. Yet it had been difficult to produce largerparticles of this 75%-sand product using existing technology.

It is the object of the present invention to resolve all of thedifficulties heretofore described.

OBJECTS OF THE INVENTION

One object of the invention is to provide an economical, industriallyfeasible process for the production of a relatively non-pollutingmagnesium calcium acetate deicer.

It is a further object to produce a low-cost magnesium acetate productsuitable for use as a deicer, and for other end uses.

Yet another object is to produce a relatively non-friable magnesiumcalcium acetate product which can be successfully stored, shipped, anddispensed.

A further object of the invention is to provide a manufacturing processfor making magnesium calcium acetate which requires a minimum ofprocessing energy for process drying.

Another object is an embodiment of a magnesium calcium acetatemanufacturing process which requires no drying step.

A further object of the invention is to provide a unique magnesiumcalcium acetate composition of matter which epitomizes favorableprocessing as well as product characteristics.

Another object is to produce a superior line of magnesium calciumacetate products by reacting the appropriate ore-blend with acetateacid, which rection is characterized by the absence of recycle streams,waste products, co-products, or by-products.

Yet another object is to produce a series of magnesium calcium acetateproducts which resist degradation in high temperature, high humidityenvironment.

A further object of this invention is to provide superior, relativelynon-polluting, and relatively non-corrosive deicers/anti-icers.

It is also an object of this invention the introduction of acoarse-particle magnesium calcium acetate product incorporatingrelatively high levels of sand or other traction agent.

A further object is to provide a relatively rapidly dissolving magnesiumcalcium acetate for commerce.

SUMMARY OF THE INVENTION

In general, mixtures or blends of finely divided dolomitic lime andmagnesium oxide are treated with a critically controlled amount ofwater, the whole then reacted with glacial acetic acid. Mixtures of oresother than the ores named will be suitable to the process providing theyprovide the desired levels of chemically reactive MgO and CaO. Also,dilute acetic acid can be used, and reacted directly with the dry oreblend.

I have discovered that the amount of input water, as in the prior art,is critically important to the success of this low-cost processingscheme. But two very important departures have been discovered:

1. A greater amount of input water is required than had heretofore beenpracticed when operating at higher values of X_(Mg), and

2. The amount of input water must be adjusted according to the molfraction X_(Mg) of magnesium desired in the product.

Thus there is not a single reaction formula, but a continuously varyingone depending upon the X_(Mg) value desired in the product, i.e.,depending on the active MgO/CaO ratio in the ore blend selected.

Furthermore it has been discovered that ore utilization is enhancedwhenever the ore is first comingled with the water required. Betterresults are obtained this way than if all required water were added tothe glacial acetic acid, so as to form an acid solution reactant. Evenat an X_(Mg) value of 1.0, where the product is straight magnesiumacetate, it can be shown that virtually all of the active MgO reactantis converted whenever 1. just sufficient water is introduced which leadsto a solid product, and 2 that water is first added to the ore, blendingwell, prior to introduction of concentrated acetic acid.

Water introduced to the ore does not slake the MgO component, as this isknown to take a matter of weeks at room temperature. Neither does itslake the CaO component as evidenced by the absence of exotherm. The CaOcomponent doesn't slake for two reasons: insufficient time is allowedfor slaking to initiate, and the presence of MgO functions as a diluentand heat absorber, thus inhibiting the CaO slaking process from takingoff.

I have thus found that when five mols of water, including the waterproduced by the chemical reaction between ore and acid, are introducedper mol of input MgO, the reaction scheme is successful in producing asolid product. For example, ##STR1## In this case there are two mols ofinput MgO, requiring a total of ten mols input water. But 3 of thesemols of water emanate from the acetic acid. Thus only 7 mols of liquidwater are actually introduced.

The procedure is to blend the dolomitic lime and MgO thoroughly, then tomix this blend in turn with all the required water. This is why the oreand water are included in the same brackets. Wetted ore and glacial (inthis case) acetic acid are then combined with agitation to form theproduct batch. Note that in this example the value of X_(Mg) is 0.67.The product consists of 2 mols of (hydrated) magnesium acetate to everymol of calcium acetate.

At the value of X_(Mg) in the example, the immediate product has aputty-like consistency which spontaneously freezes into a relativelyhard material. The freezing is a chemical process whereby the moltenmagnesium acetate converts to a crystalline hydrate. Such materialbecomes even harder when allowed to stand and lose a small fraction ofits water by air-drying. Industrially, air-drying is not feasible; a lowtemperature drying can be introduced which avoids melting of magnesiumacetate tetrahydrate, i.e., operates well below 70° C.

When the value of X_(Mg) approaches 1.0, the reaction batch increasinglygoes through a viscous phase. Indeed, at X_(Mg) =1, no insolubles arepresent, and the batch is a near-transparent viscous liquid. Theseintermediate states also spontaneously freeze to form a solid product.In general, these products require a curing during which the solidparticles become much harder, or they require a slight drying in orderto become rock hard.

There is however, a unique occurrence at and near X_(Mg) =0.80 where thereaction batch goes through a viscous phase to produce a product whichis extremely hard without curing or drying. This product contains 4 molsof hydrated magnesium acetate per mol of calcium acetate. It coulddouble as traction agent and deicer/anti-icer.

Note that all of the input water does not end up in the product. This isdue to the reaction exotherm, even at X_(Mg) =1. Thus, in the process ofinvention, 5 mols of water are introduced for every mol of magnesiumacetate product formed. Some water is evolved in processing, such thatsomething approximating 4 mols of water end up in the product relativeto mols of magnesium acetate. In this case, X_(mg) =1, it is very clear(Example I) that a lower water input level results in an incompleteutilization of MgO.

The amount of acetic acid introduced is generally the stoichiometriceqivalent of the active CaO, MgO content of the ore blend. Under thiscondition, solution of the product in water (10%, anhydrous productbasis) would approximate 7.2 in pH. If a lower or higher pH in theproduct solution is required, the ore/acid ratio can be slightlyaltered. For end use as a decier, the preferred pH range is 8-9. in thiscase a slight excess of ore is required. The solution of such a productin water exhibits a turbidity due to excess base. It is suspected thatsuch turbidity arises through the formation of relatively insolublebasic acetates.

The actual processing of intermediate stages of the product of thisinvention can proceed in a number of ways, depending upon the value ofX_(Mg). When X_(Mg) equals unity, processing proceeds in exactly thesame manner as in the production of aluminum sulfate world-wide. Here aviscous, hot product solution is poured onto a flat surface where itultimately freezes. The frozen material is then mechanically broken upand fed to conventional crushers.

Alternatively, raw material ore, water and acid streams aresimultaneously introduced to an agitated vessel containing an existingbed of crystalline product. Commercial disc or drum pelletizers aresuitable for the purpose. A somewhat more flexible commercial unit isknown as a horizontal pelletizer; in this case, raw material streams canbe introduced at selected points along the horizontal flow of materials.The horizontal pelletizer is especially useful when it is required tointroduce a traction agent such as sand into the magnesium calciumacetate product.

Individual cases may require modification of the basic equipment inorder to manufacture under optimal conditions. For example, a so-calledre-roll device is used following the drum pelletizer stage in order toprevent the product from growing beyond the specified particle size. There-roll device permits continuation of the chemical reaction, includingcrystallization or freezing, without introducing additional rawmaterial. It is thus a special way of increasing product residence time.

The time period for an intermediate stage to freeze depends upon anumber of variables. It is therefore impossible to give specific numberswithout at the same time specifying a number of other parameters.

The factors which influence freezing can be generally described asfollows:

1. Peak Temperature of the Reaction Batch--In general, the higher thetemperature allowed to be approached as a result of the reactionexotherm, the longer the batch will take to freeze.

2. Temperature of the Reaction Batch--With peak temperature specified,the longer the system is kept hot, the longer it will take to freeze.

3. Presence of Surface Active Agents--When lignosulfonates are used tohelp disperse the ore into the water, or used as binders, theintermediate stages require greater time to freeze.

4. Intoduction of Foreign Materials--Introduction of dry sand tointermediate reaction stages has been found to promote freezing. Whetherthis is due to the (slight) thermal shock, or to a nucleation process isundetermined.

5. The value of X_(Mg) --At X_(Mg) =0.67 the reaction intermediate took57 minutes to freeze. Under similar conditions, a X_(Mg) =1.0 batchrequired 100 minutes. An intermediate X_(Mg) product having a value of0.8 started freezing at 47 minutes, and completed the freezing processat 72 minutes. In all cases, neither product crystals, sand, nor surfaceactive agents were introduced. When dry sand is introduced, freezingtimes can be reduced to 1 or 2 minutes. When lignosulfonate isintroduced, freezing times can be extended to more than 8 hours. Thus,use of lignosulfonates or other surface active agents can be used tocontrol freezing, so desired.

For example, in the industrial process requiring the pouring of viscousliquid onto a flat surface, surface active agents can be used to preventpremature freezing from spurious causes.

The incorporation of sand or other traction agent into magnesium calciumacetate products of this invention is very important when the productsare to be used as deicers/anti-icers. In general, the more sandintroduced as a fraction of the product the more difficult it is toproduce a large (pea-size) product particle. At the 75% sand level, forexample, the product at a lower level of X_(Mg) tends to be smaller ofparticle size, and is actually little more than coated sand. At X_(Mg)=1 the product also tends towards a finer grained product because thecohesive forces within hydrated magnesium acetate are not great. Theseproblems have been solved by the use of lignosulfonate binder.

However, an unanticipated result was discovered at X_(Mg) =0.8. Here theintermediate stage of reaction was plastic, and was mechanicallytransformed into large particles which froze within 22 minutes of acidintroduction. No drying was required to yield a strong, nonfriableproduct. No binder or dispersant was used. In this case, wet sand andore were premixed, and acid was added to the whole.

DESCRIPTION OF PREFERRED EMBODIMENTS

The following examples will illustrate the embodiments of the invention:

EXAMPLE I

A. Illustrating Use of Insufficient Water Input. X_(Mg) =1.00

    {MgO+3H.sub.2 O}+2HAc→Product.

300 parts MgO, 98% assay, were added to 394 parts of water, and themixture thoroughly blended. To this blend were added 876 parts ofglacial acetic acid, with stirring. A clear viscous liquor was formedwhich contained many small white specks. In 23 minutes the batch hadcooled to room temperature, and there was no odor of acetic acid overthe batch. In 122 minutes from the time of acid introduction, freezingautonomously occurs. There is a strong emanation of acetic acid odor atthis point, signalling partial decomposition of the acid-acetate.

The frozen mass was mechanically broken into clumps. One day later therewas still a strong acid odor over the batch.

B. Illustrating Use of Sufficient Water Input. X_(Mg) =1.00

    {MgO+4H.sub.2 O}+2HAc→Product

300 parts MgO were added to 536 parts water, and the mixture thoroughlyblended. To this blend were added 876 parts of glacial acetic acid, withstirring. A clear viscous liquor was formed with no white particlesvisible. At 100 minutes from the time of acid introduction, the massbecame crystalline accompanied by an exotherm. No odor of acid wasevident. Product was broken into clumps which were semi-hard. Clumpswere equilibrated with atmospheric air at about 52% relative humidityand 60° F., and were thus transformed into hard particles suitable forcommerce.

Product composition is Mg(Ac)₂.3.91H₂ O. The pH of a 10% solutions is7.2. There is virtually no solid residue, and a very minor amount ofwhite flocculant solids.

EXAMPLE II

A. Illustrating Reaction Between Dry Ore Blend and Aqueous Acetic Acid.

    X.sub.Mg =0.67

300 parts of dolomitic lime, 96.7% assay, were thoroughly blended with124 parts MgO, 98% assay. To this dry blend was added 1463 parts ofhomogeneous acetic acid solution prepared by blending 1084 parts ofglacial acetic acid with 379 parts water. Reaction mixture wasthoroughly agitated. A putty-like non-sticky solid product formed almostimmediately.

At 96 minutes from the time of acid introduction, the product pelletswere hard at exterior surfaces only. Seven hours subsequent to this,pellets were uniformly hard throughout.

The pH of a 10% solution of product (anhydrous basis) in water was 8.8.Product dissolved fairly rapidly to produce a solution containing aminor amount of sediment, and flocculant solids which eventuallysettled.

B. Illustrating Reaction Between Wetted Ore and Glacial Acetic Acid

    X.sub.Mg =0.67

300 parts of dolomitic lime were blended with 124 parts MgO. To thisblend were added 379 parts of water, and the system thoroughly blended.To the wet blend were added 1084 parts of glacial acetic acid, withagitation. A non-sticky, putty-like solid product formed almostimmediately.

At 57 minutes from the time of acid introduction, the product froze toproduce a uniformly hard consistency material. Product was broken intosmaller chunks which were non-friable, and suitable for commerce.

The pH of a 10% solution of product was 8.8. Product solution wassimilar in appearance to that of IIA, excepting floc size was larger,and floc settled more slowly.,

Product composition is Ca(Ac)₂.2{Mg(Ac)₂.3.41-H₂ O}.

EXAMPLE III

Illustrating a Preferred Process/Product. X_(Mg) =0.8

    {CaO.MgO+3MgO+15H.sub.2 O}+10HAC→Product dolomitic lime

To a blend containing 200 parts dolomitic lime and 248 parts MgO wereadded 542 parts water, with agitation. To this wetted blend were added1205 parts glacial acetic acid, with agitation. A viscous paste wasformed which began to freeze 47 minutes after acid introduction.Freezing was complete in 72 minutes. No acetic acid odor was detectedover the batch during or after crystallization. Product is rock hard,and can only be broken up using hammer and chisel.

pH of a 10% product solution in water is 8.4. Minor amount of sedimentand settling turbidity present. 91 minutes after the sample froze theproduct weight was 91% of the input weight.

EXAMPLE IV

Illustrating a Preferred Process/Product X_(Mg) =0.8; 75% sand

200 parts dolime, 248 parts MgO, 542 parts water and 4434 parts of finebrick sand were thoroughly blended together. To this blend were added1205 parts glacial acetic sand. A non-sticky workable plastic mass wasformed almost immediately. Mass was mechanically converted to largesemi-hard aggregates. No odor of acetic acid was detected emanating fromthis batch.

At 22 minutes after introduction of acid the product was hard. Elevatedtemperature drying was unnecessary. Product suitable for commercewithout further treatment.

EXAMPLE V

Illustrating Relative Storage Stability of Hydrated Products ofInvention

X_(Mg) =0.60; % Sand=75%

A. 330 parts of dolomitic lime, 70 parts MgO, 3723 parts of fine bricksand and 282 parts water were thoroughly blended. To this blend wasadded 1003 parts glacial acetic acid, with agitation. Then 213 partswater were gradually added until good pellets could be formed withagitation. A sample of this product was heated in a 110° C. oven for 90minutes, whereupon it lost 10.4% in weight. The sample was cooled toroom temperature and stored in an 84% relative humidity environment.Pellets were extremely hard. Seventeen and one-half hours later thesample pellets lost crush strength to the degree that they were nolonger a viable article of commerce. Corresponding sample material whichhad not been oven-dried lost no strength under identical (side-by-side)storage conditions. Three days later the undried sample still retainedits crush strength. At this point the experiment was terminated.

B. Example VA. experiment was repeated. Subsequent to the acidintroduction step, however, an additional 50 parts water and 62 parts58% Calcium Lignosulfonate solution in water ("Norlig A") were slowlyadded until good pellets could be formed. Sample was split, one portionremaining unheated. The other portion was heated to virtual constantweight in a 110° C. oven; weight loss was 8.7%. After 11 hours ofstorage at a relative humidity of 82% no difference between heated andunheated pellet crush strengths could be discerned. However, seven andone-half hours later the oven-dried sample dramatically lost crushstrength. The unheated sample crush strength was undiminished.

Although this invention has been described in connection with specificforms thereof, it will be appreciated by those skilled in the art that awide variety of equivalents may be substituted for those specificelements and steps of operation shown and described herein, that certainfeatures may be used independently of other features, and that parts maybe reversed, all without departing from the spirit and scope of thisinvention as defined in the appended claims.

I claim:
 1. An economical process for the manufacture of magnesiumcalcium acetate hydrate comprising the following steps:a. introducingfinely divided ore containing chemically active calcium oxide andchemically active magnesium oxide to an agitated reaction vessel suchthat the mol fraction of magnesium in said ore falls within the range0.68-14 1.0. b. introducing to said agitation reaction vessel a measuredquantity of water such that the number of mols of water is numericallyequal to x times the number of mols of said chemically active magnesiumoxide, minus one-half the number of moles of acetic acid introducedwhere x equals 4.5-6; c. introducing to said agitated reaction vessel ameasured amount of acetic acid stoichiometrically equivalent to saidchemically active calcium oxide and chemically active magnesium oxide;d. allowing the product formed through steps a., b. and c. to freeze. 2.The process of claim 1, wherein said finely divided ore is reactedwithin said agitated reaction vessel with an acetic acid solutioncontaining said measured quantity of water and said measured amount ofacetic acid.
 3. The process of claim 1, wherein said mol fraction ofmagnesium is 0.8.
 4. The process of claim 1, wherein said mol fractionof magnesium is 1.0.
 5. The process of claim 1, wherein the value of xequals 5.0.
 6. The process of claim 5 wherein said mol fraction ofmagnesium is 0.8.
 7. The process of claim 5 wherein said mol fraction ofmagnesium is 1.0.
 8. The process of claim 1 wherein said product issubjected to a drying step.
 9. A new composition of matter, useful as assurface deicer, having the empirical formula

    mCa(Ac).sub.2.n{Mg(Ac).sub.2.wH.sub.2 O}.

where n/(m+n)is equal to 0.68-0.99, and W is equal to .[.3-4.]..Iadd.0-4.Iaddend..
 10. The composition of matter of claim 9 whereinn/(m+n) is equal to 0.8, and w equals .[.3-4.]. .Iadd.0-4.Iaddend.. 11.The process of claim 1 whereby traction agent is introduced into thereaction vessel such that fraction of traction agent, anhydrous productbasis, falls in the range of 1-75%.
 12. A new composition of matter,useful as a surface deicer, having the empirical formula

    mCa(Ac).sub.2.n(Mg(Ac).sub.2.wH.sub.2 O)

where n/(m+n) equals 0.68-1.00, w equals .[.3-4.]. .Iadd.0-4.Iaddend.,and incorporating within its mass 1-75% traction agent. .Iadd.
 13. A newcomposition of matter, useful as a surface deicer, having the empiricalformula

    m ca(Ac).sub.2.n{Mg(Ac).sub.2.wH.sub.2 O},

where n/(m+n) is equal to 0.68-0.99, and w is equal to 3-4..Iaddend..Iadd.14. The composition of matter of claim
 9. wherein n/(m+n) is equalto 0.8, and w equals 3-4..Iaddend. .Iadd.15. A new composition ofmatter, useful as a surface deicer, having the empirical formula

    m Ca(Ac).sub.2.n{Mg(Ac).sub.2. wH.sub.2 O},

where n/(m+n) equals 0.68-1.00, w equals 3-4, and incorporating withinits mass 1-75% traction agent..Iaddend.